Mrinal Saikiaab and
Lakshi Saikia
*ab
aMaterials Science Division, CSIR-North East Institute of Science and Technology, Jorhat – 785006, Assam, India. E-mail: l.saikia@gmail.com; Fax: +91 376 2370 011; Tel: +91 376 2370 081
bAcademy of Scientific and Innovative Research, Chennai, India
First published on 29th January 2016
Sulfonic acid-functionalized MIL-101(Cr) was established to be an active heterogeneous catalyst for the one-pot synthesis of 2-amino-4H-chromenes via a three-component condensation reaction between resorcinol, malononitrile and a diverse range of aromatic aldehydes in aqueous medium. Here, sulfonation of the parent MIL-101(Cr) has been carried out through a post synthetic modification (PSM) technique. The resulting MIL-101(Cr)–SO3H has been characterized by employing powder X-ray diffraction, N2 sorption, FESEM, EDS, FT-IR and TGA studies. Furthermore, the catalyst can easily be recovered and recycled without much change in catalytic activity.
Reports are available for the synthesis of amino chromene derivative over various lewis acid and base catalyst like NaOH,7 K2CO3,8 InCl3,9 TiCl4,10 MgO,11 Et3N12 and heteropolyacids. Although these catalysts display a very high activity and selectivity, yet the inherent drawback associated with these catalysts is their recovery and reusability due to their homogeneous character. Therefore, development of heterogeneous catalytic system is always a demandable task for sustainable development of chemical procedures owing to their facile recovery and reusability. A few heterogeneous system have been developed for the synthesis of 2-amino-4H-chromene employing the MCR strategy like triazine functionalized mesoporous organocatalyst (TFMO-1),13 nano-sized magnesium oxide, Mg/Al hydrotalcite, nano-structured diphosphate (Na2CaP2O7),14 tungstic acid functionalized mesoporous SBA-15.15 Moreover, Fe3O4@CS-SO3H NPs has been employed for the synthesis of 2-amino-4H-chromen-4-yl phosphonate derivatives.16
Metal–organic framework has been found to be gaining much importance owing to their potential application in the field of gas storage, separation and catalysis.17–20 In the field of heterogeneous catalysis, it plays a promising role because of its high surface area, regular and accessible pores and controllable structures. In particular, metal–organic framework like MIL-101(Cr) is observed to be a suitable candidate for catalysis perspective due to its thermal and chemical robustness,21 possess coordinatively unsaturated metal sites (CUSs) that can act as a mild Lewis acid,22 introduction of functional group through post synthetic modification (PSM) approach can be possible due to its excellent chemical stability. This chemical stability again makes this material a suitable candidate in various important applications.23–30 However, in case of ultra-stable MOFs the lack of functional and selective sites inhibits their uses in catalysis. In order to counteract this shortcoming, functionalization of MOFs has been carried out by encapsulating or loading different active sites like heteropoly acid,31–42 sulfonic acids into the matrix of MOFs via post-grafting, one-pot synthesis or premodification of organic linker with functionalized ligand.36,40,43–48 Among the different functionalized MIL-101(Cr), sulfonic acid functionalized MIL-101(Cr) is evaluated as one of the potential solid acid catalyst49 for various important organic transformations.46,47,49–53 As the mentioned chemical transformation is basically an acid catalyzed reaction, therefore we adopt a protocol of synthesizing 2-amino-4H-chromene through three component condensation reaction between resorcinol, aromatic aldehyde and malononitrile in aqueous medium utilizing MIL-101(Cr)–SO3H as solid acid catalyst. Herein we synthesized MIL-101(Cr)–SO3H by using a post synthetic modification approach54 and the material has been thoroughly characterized by PXRD, FE-SEM, XPS, N2 sorption, FT-IR and TGA studies. The catalyst shows excellent catalytic activity in short reaction time and can be recycled up to fifth catalytic cycles without much change in catalytic activity.
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Fig. 1 PXRD patterns of MIL-101(Cr) (red), MIL-101(Cr)–SO3H (black) and recovered MIL-101(Cr)–SO3H (blue). |
N2 physisorption analysis (Fig. 2) of both the bare (Fig. 2(a)) and acid functionalized MIL-101(Cr) (Fig. 2(b)) has been carried out at 77 K. MOF-101(Cr)–SO3H exhibits a similar typical type-I isotherm to that of the parent MIL-101(Cr). However, an appreciable decrease in surface area and pore volume from 2787 m2 g−1 and 1.58 cm3 g−1 to 2206 m2 g−1 and 1.27 cm3 g−1 has been observed for the functionalized MOF due to the partial blockage of cavities of the parent MOF by the sulfonic acid groups.
FE-SEM images (Fig. S2, ESI†) illustrate the preservation of the characteristic cubic symmetry of MIL-101(Cr) after incorporating the acid moiety into the mesocages. Energy-dispersive X-ray spectroscopy (EDS) (Fig. 3) analysis confirms the successful incorporation of –SO3H group into the framework while the elemental mapping of Cr, S, O elements of MIL-101(Cr)–SO3H clearly demonstrate that –SO3H group is well distributed into the cages of MIL-101(Cr). XPS spectrum (Fig. 4) also shows a good agreement with this result, exhibit a typical S2p band (Fig. 4(c)) at 168.2 eV corresponding to –SO3H group anchored with the linkers of the parent MOF. Furthermore, no change in the peak position has been observed with respect to the other elements present in the bare MIL-101(Cr) (Fig. 4(b)), establishing the conservation of the integrity of MIL-101(Cr) after the post synthetic modification.
The thermal stability of MIL-101(Cr)–SO3H (Fig. S3(a), ESI†) was analyzed through thermogravimetric analysis (TGA), operated in the temperature range from room temperature to 800 °C with a heating rate of 10 °C min−1 under N2 atmosphere. The first weight loss of 11.56% appeared below 150 °C is due to the loss of adsorbed water on MIL-101(Cr)–SO3H. The second weight loss of 7.77% appeared between 150–350 °C, may be attributed to the decomposition of sulfonic acid moiety anchored within the cages of MIL-101(Cr). The third weight loss step of 44.73% is due to the decomposition of MIL-101(Cr) framework. In addition, another weight loss step of 10.1% has been observed above 550 °C, establishing the decomposition of chromium sulphate.56
We have estimated the loading of –SO3H group on to the framework of MIL-101(Cr) by adopting a back titration method involving the addition of a standard NaOH solution (0.01 N) to a known quantity of MIL-101(Cr)–SO3H. After treating with NaOH, it has been assumed that all the –SO3H groups are converted into –SO3− Na+ form and the excess NaOH left in the solution is allowed to titrated with a known strength of oxalic acid (0.01 N). From the titrametric experiment it may easily be estimated the exact amount of NaOH consumed during the titration or the equivalent amount of –SO3H group attached with the linkers of MIL-101(Cr). The result shows that 1 g of MIL-101(Cr)–SO3H contains 0.15 mmol –SO3H group.
We have explored the catalytic activity of the synthesized MIL-101(Cr)–SO3H in a three component condensation reaction between aromatic aldehydes, resorcinol and malononitrile in an aqueous medium. In presence of bare MIL-101(Cr), a low yield of desired product was formed confirming the need of strong acid moiety on the framework structure to perform the condensation reaction. The effect of different dosage of the catalyst on the mentioned condensation reaction has been monitored by taking the condensation between benzaldehyde, resorcinol and malononitrile as a model reaction. From the result (Table 1) it was observed that with increase in the mol% of the catalyst (Entry 1 and 2 Table 1), the yield of the product increases with the maximum yield of 82% was obtained when the reaction was carried out with 0.37 mol% catalyst (Entry 3, Table 1). This may be due to the increase in the number of active sites on the catalyst with increase in catalyst dosage. No significant increase in product yield was obtained with further increase in the mol% of the catalyst (Entry 4, Table 1), therefore, 0.37 mol% catalyst has been considered as the optimum catalyst amount to conduct the three component condensation reaction.
The solvent effect on the condensation reaction between benzaldehyde, resorcinol and malononitrile has been studied by carry out the reaction in various types of solvents exhibit different polarities under reflux condition. From the result (Table S1, ESI†) it has been concluded that the desired product formation in polar protic solvents like ethanol, methanol and water (Entry 1, 2 and 4, Table S1, ESI†) was found to much higher than that of the polar aprotic solvent like acetonitrile, THF, DCM, (Entry 3, 5 and 6, Table S1, ESI†) where we have observed the Knoevenagel condensation adduct as the major product. This behaviour may be attributed to the more polar character of the product to that of reactant molecules. However, under solvent free condition (Entry 7, Table S1, ESI†) the desired product yield was found to be low that clearly demonstrate that water is the suitable solvent (Entry 4, Table S1, ESI†) for carrying out the three component condensation reaction that furnish the highest yield of the product under the optimized condition.
The influence of the temperature on the one pot three component condensation reaction between benzaldehyde, resorcinol and malononitrile has been invested (Table 2). The results show that at room temperature the reaction cannot proceed even running the reaction for 12 h, while with increase in temperature (Entry 2, 3 and 4, Table 2) the amount of desired product increases with a maximum yield 82% was obtained at 100 °C (Entry 5, Table 2). We have also found a very low yield of the desired product in the absence of catalyst at 100 °C, owing to the thermal condensation reaction at higher temperature. Therefore, taking all these aspects we have chosen 100 °C as the optimum temperature to carry out the further studies.
The substrate scope of the catalyst has been examined by employing various aromatic aldehydes containing electron-withdrawing, electron donating substituents. The results are summarized in Table 3. It has been observed that MIL-101(Cr)–SO3H is very active to all kind of aromatic aldehydes. In fact, we do not observe any pronounced substituent effect attached to the phenyl ring over the reaction as both the electron withdrawing (Entry 8–10, Table 3) and donating groups (Entry 2–7, Table 3) show the condensation reaction with almost equal efficiencies. However, ortho substituted aldehydes display a lower yield of product as compared to its meta and para analogues, may be ascribed to the electronic effect. In addition, the heteroaromatic aldehydes like pyridine-2-carbaldehyde (Entry 11, Table 3) furan-2-carbaldehyde (Entry 12, Table 3) are also quite compatible with this present catalytic system. Overall MIL-101(Cr)–SO3H has been established to be a highly flexible catalyst for the proposed one-pot three component condensation reaction.
Entry | Aromatic aldehydes | Time (h) | Product | Yieldb (%) |
---|---|---|---|---|
a Reaction conditions: aromatic aldehydes (1 mmol), resorcinol (1 mmol), malononitrile (1 mmol), water = 5 ml, MIL-101(Cr)–SO3H (0.37 mol%).b Isolated yields are based on aromatic aldehydes. All compounds have been characterized by 1H and 13C NMR (available in the ESI). | ||||
1 | ![]() |
3 | 2a | 82 |
2 | ![]() |
7 | 2b | 76 |
3 | ![]() |
7 | 2c | 78 |
4 | ![]() |
4 | 2d | 80 |
5 | ![]() |
4.5 | 2e | 78 |
6 | ![]() |
3.5 | 2f | 80 |
7 | ![]() |
3.5 | 2g | 76 |
8 | ![]() |
3 | 2h | 81 |
9 | ![]() |
4 | 2i | 74 |
10 | ![]() |
3.5 | 2j | 77 |
11 | ![]() |
6 | 2k | 72 |
12 | ![]() |
7 | 2l | 70 |
The efficiency of the present catalytic system has been examined by taking the condensation reaction between 4-chlorobenzaldehyde, resorcinol and malononitrile as the representative case. From the results (shown in Table S2, ESI†) it has been observed that most of the catalysts available in the literature are homogeneous in nature that displays the basic shortcoming of their recovery and reusability. The prime advantages of our protocol are high product yield%, facile recovery and reusability, low catalyst dosage, high TON etc. Furthermore, the high surface area of the material provides a better dispersion of catalytically active sites that actually increases the yield of the product.
A plausible reaction mechanism has been proposed based on the available literature and our experimental data. Actually, the reaction was proceed through Knoevenagel condensation reaction between aromatic aldehyde and malononitrile followed by Michael addition of resorcinol with the Knoevenagel product ((I) Scheme 1). The final step of the reaction is an intra-molecular cyclization ((II) Scheme 1) and tautomerization to afford the desired 2-amino-4H-chromenes ((III) Scheme 1). The catalyst MIL-101(Cr)–SO3H containing the acid sites increases the electrophilicity of the aldehydic carbon which undergo dehydration to give the Knoevenagel product. The Cr(III) sites presented in the parent MOF may increase the electrophilicity of the –CN group of the Knoevenagel product to facilitate the Michael addition which subsequently undergoes intra-molecular cyclization and tautomerization to yield the 2-amino-4H-chromene derivative.
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Scheme 1 Plausible reaction mechanism for the condensation reaction between aromatic aldehyde, resorcinol and malononitrile in the presence of MIL-101(Cr)–SO3H. |
The heterogeneous nature of MIL-101(Cr)–SO3H was examined by performing a hot filtration test involving the reaction between benzaldehyde, resorcinol and malononitrile under the optimized reaction condition. After 1 h of the reaction the catalyst was removed from the reaction mixture by filtration (product yield 40%) and allowed the reaction to proceed with the filtrate for further 2 h. No increase in the product yield beyond 40% was observed after 2 h reaction time. This result clearly confirms the heterogeneous nature of MIL-101(Cr)–SO3H during the course of the reaction.
The reusability of the catalyst was monitored by taking the condensation reaction between benzaldehyde, resorcinol and malononitrile as the model reaction. After completion of the reaction the catalyst was recovered from the reaction mixture through filtration, washed it with acetone for several times and then dried in an oven at 70 °C for 3 h. The activated MIL-101(Cr)–SO3H was then subsequently employed for the next catalytic run under identical condition. The results (Fig. 5) show that the catalyst can perform effectively up to fifth catalytic cycle without any significant loss of its catalytic activity. The crystallinity of the recovered catalyst is well maintained as indicated by the PXRD analysis (Fig. 1 (blue)). FT-IR analysis (Fig. S1(c)†) also shows a good agreement with the PXRD results. The vibrational bands corresponding to the bare MIL-101(Cr) is well preserved in the recovered catalyst. FE-SEM image of the recovered catalyst (Fig. S2(c)†) clearly demonstrate the preservation of the integrity of the parent MOF. We have calculated the S content of the recovered catalyst and it was found to be 0.10 mmol g−1. All these results strongly recommend that a heterogeneous process was involved in the mentioned organic transformation and also establishing the chemical robustness of the catalyst.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c5ra28135k |
This journal is © The Royal Society of Chemistry 2016 |